US4786666A - Epoxy compositions containing glycidyl ethers of fatty esters - Google Patents

Epoxy compositions containing glycidyl ethers of fatty esters Download PDF

Info

Publication number
US4786666A
US4786666A US07/122,060 US12206087A US4786666A US 4786666 A US4786666 A US 4786666A US 12206087 A US12206087 A US 12206087A US 4786666 A US4786666 A US 4786666A
Authority
US
United States
Prior art keywords
composition
dihydric phenol
acid
weight
diglycidyl ether
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
US07/122,060
Inventor
Joseph L. Cecil
Walter J. Kurnik
Donald E. Babcock
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Shell USA Inc
Original Assignee
Interez Inc
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Interez Inc filed Critical Interez Inc
Priority to US07/122,060 priority Critical patent/US4786666A/en
Assigned to INTEREZ, INC., A CORP. OF GA reassignment INTEREZ, INC., A CORP. OF GA ASSIGNMENT OF ASSIGNORS INTEREST. Assignors: KURNIK, WALTER J., BABCOCK, DONALD E., CECIL, JOSEPH L.
Priority to CA000581708A priority patent/CA1328529C/en
Application granted granted Critical
Publication of US4786666A publication Critical patent/US4786666A/en
Assigned to HI-TEK POLYMERS, INC. reassignment HI-TEK POLYMERS, INC. MERGER (SEE DOCUMENT FOR DETAILS). Assignors: INTEREZ, INC.
Assigned to SHELL OIL COMPANY reassignment SHELL OIL COMPANY ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: HI-TEK POLYMERS, INC.
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G59/00Polycondensates containing more than one epoxy group per molecule; Macromolecules obtained by polymerising compounds containing more than one epoxy group per molecule using curing agents or catalysts which react with the epoxy groups
    • C08G59/02Polycondensates containing more than one epoxy group per molecule
    • C08G59/04Polycondensates containing more than one epoxy group per molecule of polyhydroxy compounds with epihalohydrins or precursors thereof
    • C08G59/06Polycondensates containing more than one epoxy group per molecule of polyhydroxy compounds with epihalohydrins or precursors thereof of polyhydric phenols
    • C08G59/066Polycondensates containing more than one epoxy group per molecule of polyhydroxy compounds with epihalohydrins or precursors thereof of polyhydric phenols with chain extension or advancing agents
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G59/00Polycondensates containing more than one epoxy group per molecule; Macromolecules obtained by polymerising compounds containing more than one epoxy group per molecule using curing agents or catalysts which react with the epoxy groups
    • C08G59/14Polycondensates modified by chemical after-treatment
    • C08G59/1433Polycondensates modified by chemical after-treatment with organic low-molecular-weight compounds
    • C08G59/1438Polycondensates modified by chemical after-treatment with organic low-molecular-weight compounds containing oxygen
    • C08G59/1455Monocarboxylic acids, anhydrides, halides, or low-molecular-weight esters thereof
    • C08G59/1461Unsaturated monoacids
    • C08G59/1472Fatty acids
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G59/00Polycondensates containing more than one epoxy group per molecule; Macromolecules obtained by polymerising compounds containing more than one epoxy group per molecule using curing agents or catalysts which react with the epoxy groups
    • C08G59/18Macromolecules obtained by polymerising compounds containing more than one epoxy group per molecule using curing agents or catalysts which react with the epoxy groups ; e.g. general methods of curing
    • C08G59/20Macromolecules obtained by polymerising compounds containing more than one epoxy group per molecule using curing agents or catalysts which react with the epoxy groups ; e.g. general methods of curing characterised by the epoxy compounds used
    • C08G59/32Epoxy compounds containing three or more epoxy groups
    • C08G59/38Epoxy compounds containing three or more epoxy groups together with di-epoxy compounds
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G59/00Polycondensates containing more than one epoxy group per molecule; Macromolecules obtained by polymerising compounds containing more than one epoxy group per molecule using curing agents or catalysts which react with the epoxy groups
    • C08G59/18Macromolecules obtained by polymerising compounds containing more than one epoxy group per molecule using curing agents or catalysts which react with the epoxy groups ; e.g. general methods of curing
    • C08G59/40Macromolecules obtained by polymerising compounds containing more than one epoxy group per molecule using curing agents or catalysts which react with the epoxy groups ; e.g. general methods of curing characterised by the curing agents used
    • C08G59/42Polycarboxylic acids; Anhydrides, halides or low molecular weight esters thereof
    • C08G59/4292Polycarboxylic acids; Anhydrides, halides or low molecular weight esters thereof together with monocarboxylic acids

Definitions

  • the field of art to which this invention pertains is polymers derived from polyepoxide resins and fatty acids.
  • Epoxy esters are well known compositions which have been used industrially and in home maintenance for many years.
  • Epoxy esters are made by reacting a polymeric epoxy resin, which contains both epoxy groups and hydroxyl groups, with fatty acids.
  • the polymeric epoxy resin is made "in situ" by the reaction of a low molecular weight diepoxide with a dihydric phenol.
  • Epoxy esters are described in a large number of patents, examples of which are U.S. Pat. Nos. 2,456,408; 2,493,386; 2,698,308 and 3,247,136.
  • the esters are usually dissolved in an organic solvent at a resin solids content of 50 weight percent or less. Due to environmental concerns, there is a continuing effort to decrease the amount of solvent released to the atmosphere by increasing the solids content of coating composition.
  • This invention is directed to epoxy ester composition.
  • this invention pertains to a modified epoxy ester composition.
  • this invention relates to high solids epoxy ester coating compositions.
  • the epoxy ester composition of this invention is the reaction product of (a) a diglycidyl ether of a dihydric phenol; (b) castor oil polyglycidyl ether; (c) a dihydric phenol; (d) a monocarboxylic fatty acid; and (e) a dimer acid.
  • the diglycidyl ether of the dihydric phenol, the castor oil polyglycidyl ether and the dihydric phenol are reacted in such amounts that the sum of the epoxide equivalents of the diglycidyl ether of the dihydric phenol and the caster oil polyglycidyl ether and the phenolic equivalents of the dihydric phenol are in the ratio of about 2:1 to about 4:3.
  • About 70 to about 80 percent of the epoxide equivalents are derived from the diglycidyl ether of the dihydric phenol with the remainder being derived from the castor oil polyglycidyl ether.
  • the monocarboxylic fatty acid is present in the amount of about 26 to about 42 weight percent and the dimer acid is present in the amount of about 4 to about 8 weight percent, said weight percents being based on the total weight of the components referred to hereinabove.
  • the diglycidyl ethers of dihydric phenols useful in this invention are well known in the art. These glycidyl ethers are made by reacting a dihydric phenol with epichlorohydrin, generally in excess, using caustic as the condensation and dehydrohalogenation agent.
  • the dihydric phenols used in making the glycidyl ethers contain two phenolic hydroxyl groups and no other groups reactive under the conditions of reactions.
  • dihydric phenols examples include resorcinol, dihydroxydiphenyl, dihydroxydiphenyl ether, dihydroxydiphenyl methane, dihydroxydiphenyl ethane, p,p'-dihydroxydiphenyl propane (or Bisphenol A as it is commonly called), p,p'-dihydroxydiphenyl sulfone and the like.
  • diglycidyl ethers will have epoxide equivalent weights of about 120 to about 300.
  • a preferred diglycidyl ether is the diglycidyl ether of Bisphenol A having an epoxide equivalent weight of about 180 to about 200.
  • the castor oil polyglycidyl ether useful in this invention is the reaction product of castor oil and epichlorohydrin.
  • Castor oil is a vegetable oil obtained from the seeds of the castor plant and is the triester of glycerl and substantially ricinoleic acid.
  • Epichlorohydrin is reacted with the hydroxyl groups in the ricinoleic acid portion of the oil using a Lewis acid catalyst.
  • the resulting chlorohydrin adduct is dihydrohalogenerated with caustic.
  • Castor oil polyglycidyl ether is described in detail in U.S. Pat. No. 3,351,574, which is hereby incorporated by reference.
  • Castor oil polyglycidyl ether useful in this invention has an epoxide equivalent weight of about 550 to about 700.
  • dihydric phenols useful in this invention are those which are listed hereinbefore in the description of the diglycidyl ether of a dihydric phenol.
  • the preferred dihydric phenol is Bisphenol A.
  • the monocarboxylic fatty acids useful in this invention are aliphatic acids which contain from about 10 to about 22 carbon atoms.
  • the acids can be saturated or unsaturated with one to three ethylenically unsaturated groups per molecule.
  • examples of such acids are capric acid, lauric acid, myristic acid, palmitic acid, stearic acid, arachidic acid, behenic acid, oleic acid, linoleic acid, linolenic acid, eleostearic acid, licanic acid and erucic acid.
  • Such acid are also named from the oils from which they are derived, such as coconut fatty acids, corn oil fatty acids, linseed fatty acids, soybean fatty acids, tall oil fatty acids and the like.
  • Epoxy esters which are used to prepare coating composition which dry or cure by air oxidation, are made with unsaturated fatty acids.
  • Coating compositions which are cured with crosslinkers, such as urea-formaldehyde and melamine-formaldehyde resins, are made from epoxy esters which contain less or no unsaturation in the fatty acid portion.
  • Preferred fatty acids for use in this invention are tall oil fatty acids.
  • the dimer acids useful in this invention are dimers of unsaturated fatty acids, such as linoleic acid, linolenic acid, eleostearic acid and the like. Such acids contain an average of about 20 to about 44 carbon atoms per molecule. Although referred to as dimer acids, the compounds are mixtures of dimers and trimers with a small amount of monomer. Generally, the mixture contains at least about 80 weight percent dimer acids and about 2 to about 5 weight percent monomer with the remainder being trimer. Dimer acids are described in U.S. Pat. No. 2,482,761 which is hereby incorporated by reference.
  • the backbone epoxy resin which is esterified with the fatty acids is prepared by reacting the diglycidyl ether of the dihydric phenol and the castor oil polyglycidyl ether with a dihydric phenol in the equivalent ration of about 2 epoxide equivalents to one phenolic equivalent to about 4 epoxide equivalents to three phenolic equivalents.
  • the epoxide equivalent weight of the backbone resin, if isolated, is about 500 to about 1200.
  • a preferred epoxide equivalent weight is about 750 to about 900.
  • the backbone epoxy resin is prepared by heating the components at temperature of about 350° F. to about 500° F. for a time sufficient for the reaction to be completed as determined by the epoxide equivalent weight compared it to the calculated value.
  • Catalysts typically used in "upgrade” reactions i.e., the reaction of low molecular weight diepoxides with dihydric phenols to make higher molecular weight epoxides, are used in this reactin.
  • Examples of such catalysts are lithium hydroxide, sodium hydroxide, potassium hydroxide, sodium carbonate, triphenylphosphine, the "onium”, “sulfonium” and “phosphonium” compounds, e.g., tetramethylammonium chloride, and the like. The use of these catalysts are well known to those skilled in the art.
  • esterification catalysts e.g., sodium benzoate. Heating is conducted at a temperature of about 325° F. to about 550° F. to complete the esterification reaction.
  • a small amount of organic solvent which forms an azeotrope with water is added. Any of the aliphatic or aromatic hydrocarbons can be used. A preferred solvent is xylene.
  • the esterification reaction is conducted until the acid value measures less than 10.
  • dimer acids are added and the esterification reaction is continued until the acid value is reduced to below 10, preferably 2.5.
  • the amount of fatty monocarboxylic acid used in preparing the compositions is about 26 to about 42 weight percent based on the total weight of the composition.
  • the amount of dimer acids used is about 4 to about 8 weight percent based on the total weight of the composition.
  • Preferred amounts are about 30 to about 38 weight percent fatty monocarboxylic acid and about 5 to about 7 weight percent dimer acids.
  • Solvent solutions of the epoxy esters of this invention are formulated into coating compositions. It has been found that these castor oil polyglycidyl ether modified epoxy esters of this invention can be formulated into coatings having high solids at application viscosities.
  • the compositions of this invention can be supplied to formulators at solids contents as high as 80 percent with viscosities of less than Z on the Gardner-Holdt scale. These solids and viscosities allow formulators to make varnishes and paints with low amounts of volatile solvents which enable them to meet various environmental laws pertaining to solvent emissions.
  • Solvents used with the epoxy esters of this invention are hydrocarbon solvents, e.g., toluene, xylene, and naphtha, alcohols, glycol ethers and ketones.
  • a preferred solvent is xylene.
  • compositions of this invention can be formulated into air-drying and baking varnishes and enamels.
  • Air-drying compositions will contain driers such as cobalt and manganese naphthenate, which are well known in the art.
  • Baking compositions can also contain driers as well as crosslinking additives, such as urea-formaldehyde and melamine-formaldehyde resins.
  • paints and varnishes various other components, such as pigments, anti-skinning agents and anti-flooding compounds, can be added.
  • Example 2 Using the same procedure described in Example 1, an epoxy ester, which contained no castor oil polyglycidyl ether modification, was made from 43.21 parts of the diglycidyl ether of Bisphenol A described in Example 1, 17.65 parts of Bisphenol A, 33.72 parts of tall oil fatty acids and 6.85 parts of dimer acids as described in Example 1. The resulting ester, when dissolved at 50 percent solids in xylene, had a Gardner-Holdt viscosity at 25° C. of X-Y.
  • a clear coating composition was prepared from the epoxy ester solution of Example 1 by adding cobalt naphthenate and manganese naphthenate driers in the amount of about 0.156 percent cobalt and 0.078 percent manganese, both as metal based on ester solids. The solution was reduced to 70 percent solids with xylene to an application viscosity of 76 KU s .
  • a clear coating composition was also prepared from Example 2. Reduction to application viscosity of 89 KU s was 41.2 percent solids.
  • Films prepared from the coating composition made from Example 1 were tracked free in 6 to 24 hours and developed a pencil hardness of less than 6B in two weeks.
  • the solvent resistance, methyl ethyl ketone double rubs, was 12 after two weeks.
  • Comparable films made from the Example 2 epoxy ester were tack free in 3 hours and developed pencil hardness of HB after two weeks.
  • the solvent resistance after two weeks was 6 methyl ethyl ketone double ribs.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Organic Chemistry (AREA)
  • Emergency Medicine (AREA)
  • General Chemical & Material Sciences (AREA)
  • Epoxy Resins (AREA)
  • Paints Or Removers (AREA)

Abstract

Epoxy esters which are formulated into high solids coating compositions are made from epoxy resins and fatty acids wherein the epoxy resin is made from a diglycidyl ether of a dihydric phenol and castor oil polyglycidyl ether reacted with a dihydric phenol.

Description

BACKGROUND OF THE INVENTION
The field of art to which this invention pertains is polymers derived from polyepoxide resins and fatty acids.
Coating compositions made from epoxy esters are well known compositions which have been used industrially and in home maintenance for many years. Epoxy esters are made by reacting a polymeric epoxy resin, which contains both epoxy groups and hydroxyl groups, with fatty acids. In some instances, the polymeric epoxy resin is made "in situ" by the reaction of a low molecular weight diepoxide with a dihydric phenol. Epoxy esters are described in a large number of patents, examples of which are U.S. Pat. Nos. 2,456,408; 2,493,386; 2,698,308 and 3,247,136.
In formulating epoxy esters into coating compositions, the esters are usually dissolved in an organic solvent at a resin solids content of 50 weight percent or less. Due to environmental concerns, there is a continuing effort to decrease the amount of solvent released to the atmosphere by increasing the solids content of coating composition.
SUMMARY OF INVENTION
This invention is directed to epoxy ester composition. In one aspect, this invention pertains to a modified epoxy ester composition. In another aspect, this invention relates to high solids epoxy ester coating compositions.
The epoxy ester composition of this invention is the reaction product of (a) a diglycidyl ether of a dihydric phenol; (b) castor oil polyglycidyl ether; (c) a dihydric phenol; (d) a monocarboxylic fatty acid; and (e) a dimer acid. The diglycidyl ether of the dihydric phenol, the castor oil polyglycidyl ether and the dihydric phenol are reacted in such amounts that the sum of the epoxide equivalents of the diglycidyl ether of the dihydric phenol and the caster oil polyglycidyl ether and the phenolic equivalents of the dihydric phenol are in the ratio of about 2:1 to about 4:3. About 70 to about 80 percent of the epoxide equivalents are derived from the diglycidyl ether of the dihydric phenol with the remainder being derived from the castor oil polyglycidyl ether. The monocarboxylic fatty acid is present in the amount of about 26 to about 42 weight percent and the dimer acid is present in the amount of about 4 to about 8 weight percent, said weight percents being based on the total weight of the components referred to hereinabove.
DESCRIPTION OF THE INVENTION
The diglycidyl ethers of dihydric phenols useful in this invention are well known in the art. These glycidyl ethers are made by reacting a dihydric phenol with epichlorohydrin, generally in excess, using caustic as the condensation and dehydrohalogenation agent. The dihydric phenols used in making the glycidyl ethers contain two phenolic hydroxyl groups and no other groups reactive under the conditions of reactions. Examples of such dihydric phenols include resorcinol, dihydroxydiphenyl, dihydroxydiphenyl ether, dihydroxydiphenyl methane, dihydroxydiphenyl ethane, p,p'-dihydroxydiphenyl propane (or Bisphenol A as it is commonly called), p,p'-dihydroxydiphenyl sulfone and the like. Such diglycidyl ethers will have epoxide equivalent weights of about 120 to about 300. A preferred diglycidyl ether is the diglycidyl ether of Bisphenol A having an epoxide equivalent weight of about 180 to about 200.
The castor oil polyglycidyl ether useful in this invention is the reaction product of castor oil and epichlorohydrin. Castor oil is a vegetable oil obtained from the seeds of the castor plant and is the triester of glycerl and substantially ricinoleic acid. Epichlorohydrin is reacted with the hydroxyl groups in the ricinoleic acid portion of the oil using a Lewis acid catalyst. The resulting chlorohydrin adduct is dihydrohalogenerated with caustic. Castor oil polyglycidyl ether is described in detail in U.S. Pat. No. 3,351,574, which is hereby incorporated by reference. Castor oil polyglycidyl ether useful in this invention has an epoxide equivalent weight of about 550 to about 700.
The dihydric phenols useful in this invention are those which are listed hereinbefore in the description of the diglycidyl ether of a dihydric phenol. The preferred dihydric phenol is Bisphenol A.
The monocarboxylic fatty acids useful in this invention are aliphatic acids which contain from about 10 to about 22 carbon atoms. The acids can be saturated or unsaturated with one to three ethylenically unsaturated groups per molecule. Examples of such acids are capric acid, lauric acid, myristic acid, palmitic acid, stearic acid, arachidic acid, behenic acid, oleic acid, linoleic acid, linolenic acid, eleostearic acid, licanic acid and erucic acid. Such acid are also named from the oils from which they are derived, such as coconut fatty acids, corn oil fatty acids, linseed fatty acids, soybean fatty acids, tall oil fatty acids and the like. Epoxy esters, which are used to prepare coating composition which dry or cure by air oxidation, are made with unsaturated fatty acids. Coating compositions which are cured with crosslinkers, such as urea-formaldehyde and melamine-formaldehyde resins, are made from epoxy esters which contain less or no unsaturation in the fatty acid portion. The use of such acids is well known in the art. Preferred fatty acids for use in this invention are tall oil fatty acids.
The dimer acids useful in this invention are dimers of unsaturated fatty acids, such as linoleic acid, linolenic acid, eleostearic acid and the like. Such acids contain an average of about 20 to about 44 carbon atoms per molecule. Although referred to as dimer acids, the compounds are mixtures of dimers and trimers with a small amount of monomer. Generally, the mixture contains at least about 80 weight percent dimer acids and about 2 to about 5 weight percent monomer with the remainder being trimer. Dimer acids are described in U.S. Pat. No. 2,482,761 which is hereby incorporated by reference.
The backbone epoxy resin which is esterified with the fatty acids is prepared by reacting the diglycidyl ether of the dihydric phenol and the castor oil polyglycidyl ether with a dihydric phenol in the equivalent ration of about 2 epoxide equivalents to one phenolic equivalent to about 4 epoxide equivalents to three phenolic equivalents. The epoxide equivalent weight of the backbone resin, if isolated, is about 500 to about 1200. A preferred epoxide equivalent weight is about 750 to about 900.
The backbone epoxy resin is prepared by heating the components at temperature of about 350° F. to about 500° F. for a time sufficient for the reaction to be completed as determined by the epoxide equivalent weight compared it to the calculated value. Catalysts typically used in "upgrade" reactions, i.e., the reaction of low molecular weight diepoxides with dihydric phenols to make higher molecular weight epoxides, are used in this reactin. Examples of such catalysts are lithium hydroxide, sodium hydroxide, potassium hydroxide, sodium carbonate, triphenylphosphine, the "onium", "sulfonium" and "phosphonium" compounds, e.g., tetramethylammonium chloride, and the like. The use of these catalysts are well known to those skilled in the art.
After the completion of the epoxide-phenol reaction, the monocarboxylic acids are added along with a small amount of esterification catalysts, e.g., sodium benzoate. Heating is conducted at a temperature of about 325° F. to about 550° F. to complete the esterification reaction. In order to facilitate the removal of water of esterification, a small amount of organic solvent which forms an azeotrope with water is added. Any of the aliphatic or aromatic hydrocarbons can be used. A preferred solvent is xylene. The esterification reaction is conducted until the acid value measures less than 10.
When the desired acid value is reached, dimer acids are added and the esterification reaction is continued until the acid value is reduced to below 10, preferably 2.5.
The amount of fatty monocarboxylic acid used in preparing the compositions is about 26 to about 42 weight percent based on the total weight of the composition. The amount of dimer acids used is about 4 to about 8 weight percent based on the total weight of the composition. Preferred amounts are about 30 to about 38 weight percent fatty monocarboxylic acid and about 5 to about 7 weight percent dimer acids.
Solvent solutions of the epoxy esters of this invention are formulated into coating compositions. It has been found that these castor oil polyglycidyl ether modified epoxy esters of this invention can be formulated into coatings having high solids at application viscosities. The compositions of this invention can be supplied to formulators at solids contents as high as 80 percent with viscosities of less than Z on the Gardner-Holdt scale. These solids and viscosities allow formulators to make varnishes and paints with low amounts of volatile solvents which enable them to meet various environmental laws pertaining to solvent emissions.
Solvents used with the epoxy esters of this invention are hydrocarbon solvents, e.g., toluene, xylene, and naphtha, alcohols, glycol ethers and ketones. A preferred solvent is xylene.
The compositions of this invention can be formulated into air-drying and baking varnishes and enamels. Air-drying compositions will contain driers such as cobalt and manganese naphthenate, which are well known in the art. Baking compositions can also contain driers as well as crosslinking additives, such as urea-formaldehyde and melamine-formaldehyde resins.
In formulating paints and varnishes, various other components, such as pigments, anti-skinning agents and anti-flooding compounds, can be added.
The following examples described the invention in more detail. Parts and percentages are by weight unless otherwise designated.
EXAMPLE 1
To a suitable reactor were added 467 parts of the diglycidyl ether of Bisphenol A having an epoxide equivalent weight of 189, 524 parts of castor oil polyglycidyl ether having an epoxide equivalent weight of 637 and 209 parts of Bisphenol A. Heat and agitation were applied raising the temperature to 200° F. Potassium hydroxide, 0.31 part of 45 percent aqueous solution, was added and the temperature was raised to 350° F. over a 20 minute period. Heating was discontinued and the temperature rose to 360° F. due to the exothermic reaction. Heat was reapplied and the temperature was raised to 400° F. Heating at 400° F. was continued for 2 hours and 15 minutes. Tall oil fatty acids, 665 parts, and sodium benzoate catalyst, 1.7 parts, were added. The temperature, which had dropped to 292° F., was raised to 325° F. and was held at this temperature for 30 minutes. Xylene, 58 parts, was added and heating was continued while distilling off the water of esterification as an azeotrope while returning water to the reactor. Heating and distillation were continued for 2 hours and 25 minutes while the reactor temperature rose to 498° F., and the acid value reached 39. Dimer acids, 135 parts, (80 percent dimer, 17 percent trimer and 3 percent monomer fatty acids) were added. Heating, with azeotropic distillation of water, was continued for one hour and 20 minutes with the temperature rising to 510° F. and the acid value reaching 2.6. Xylene, approximately 500 parts, was added to form a solution at 80 percent solids. The resulting ester solution had a Gardner-Holdt viscosity of X-Y at 25° C. and a solids content of 79.45 percent.
EXAMPLE 2
Using the same procedure described in Example 1, an epoxy ester, which contained no castor oil polyglycidyl ether modification, was made from 43.21 parts of the diglycidyl ether of Bisphenol A described in Example 1, 17.65 parts of Bisphenol A, 33.72 parts of tall oil fatty acids and 6.85 parts of dimer acids as described in Example 1. The resulting ester, when dissolved at 50 percent solids in xylene, had a Gardner-Holdt viscosity at 25° C. of X-Y.
EXAMPLE 3
A clear coating composition was prepared from the epoxy ester solution of Example 1 by adding cobalt naphthenate and manganese naphthenate driers in the amount of about 0.156 percent cobalt and 0.078 percent manganese, both as metal based on ester solids. The solution was reduced to 70 percent solids with xylene to an application viscosity of 76 KUs.
A clear coating composition was also prepared from Example 2. Reduction to application viscosity of 89 KUs was 41.2 percent solids.
Films prepared from the coating composition made from Example 1 were tracked free in 6 to 24 hours and developed a pencil hardness of less than 6B in two weeks. The solvent resistance, methyl ethyl ketone double rubs, was 12 after two weeks. Comparable films made from the Example 2 epoxy ester were tack free in 3 hours and developed pencil hardness of HB after two weeks. The solvent resistance after two weeks was 6 methyl ethyl ketone double ribs.
The principles, preferred embodiments and modes of operation of the present invention have been described in the foregoing specification. The invention which is intended to be protected herein, however, is not to be construed as limited to the particular forms disclosed, since these are to be regarded as illustrating rather than restrictive. Variations and changes may be made by those skilled in the art without departing from the spirit of the invention.

Claims (9)

What is claimed:
1. An epoxy ester composition comprising the reaction product of:
(a) a diglycidyl ether of a dihydric phenol;
(b) castor oil polyglycidyl ether;
(c) a dihydric phenol;
(d) a monocarboxylic fatty acid; and
(e) a dimer acid,
wherein the sum of the epoxide equivalents of (a) and (b) and the phenolic equivalents of (c) are in the ratio of about 2:1 to about 4:3; wherein about 70 to about 80 percent of the epoxide equivalents are derived from (a) and the remainder from (b); wherein (d) and (e) are present in the amount of about 26 to about 42 weight percent (e), said weight percents being based on the total weight of (a), (b), (c), (d) and (e).
2. The composition of claim 1 wherein:
(a) the diglycidyl ether of the dihydric phenol has an epoxide equivalent weight of about 180 to about 200, wherein
(b) the castor oil polyglycidyl ether has an epoxide equivalent weight of about 550 to about 700, wherein
(c) the monocarboxylic fatty acid contains about 10 to about 22 carbon atoms, and wherein
(d) the dimer acid is a dimer of unsaturated monocarboxylic fatty acids and contains an average of about 20 to about 44 carbon atoms per molecule.
3. The composition of claim 1 wherein (d) the monocarboxylic fatty acid and (e) the dimer acids, are present in the amount of about 30 to about 38 weight percent (d) and about 5 to about 7 weight percent (e).
4. The composition of claim 1 wherein (a), the diglycidyl ether, is a diglycidyl ether of Bisphenol A having an epoxide equivalent weight of about 180 to about 200 and (c) the dihydric phenol, is Bisphenol A.
5. The composition of claim 1 wherein (d), the monocarboxylic fatty acid, is tall oil fatty acids.
6. The composition of claim 1 wherein the reaction product of (a) the diglycidyl ether of the dihydric phenol, (b) the castor oil polyglycidyl ether and (c) the dihydric phenol before esterification with (d) the monocarboxylic fatty acid and (e) the dimer acid has an epoxide equivalent weight of about 500 to about 1200.
7. The composition of claim 6 wherein the epoxide equivalent weight is about 750 to about 900.
8. A solution of the composition of claim 1 in an organic solvent.
9. The solution of claim 8 wherein the organic solvent is xylene.
US07/122,060 1987-11-18 1987-11-18 Epoxy compositions containing glycidyl ethers of fatty esters Expired - Fee Related US4786666A (en)

Priority Applications (2)

Application Number Priority Date Filing Date Title
US07/122,060 US4786666A (en) 1987-11-18 1987-11-18 Epoxy compositions containing glycidyl ethers of fatty esters
CA000581708A CA1328529C (en) 1987-11-18 1988-10-31 Epoxy ester compositions

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US07/122,060 US4786666A (en) 1987-11-18 1987-11-18 Epoxy compositions containing glycidyl ethers of fatty esters

Publications (1)

Publication Number Publication Date
US4786666A true US4786666A (en) 1988-11-22

Family

ID=22400369

Family Applications (1)

Application Number Title Priority Date Filing Date
US07/122,060 Expired - Fee Related US4786666A (en) 1987-11-18 1987-11-18 Epoxy compositions containing glycidyl ethers of fatty esters

Country Status (2)

Country Link
US (1) US4786666A (en)
CA (1) CA1328529C (en)

Cited By (19)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0379943A2 (en) * 1989-01-23 1990-08-01 The Dow Chemical Company Process for preparation of high-molecular-weight epoxy dimer acid ester resin
US5059293A (en) * 1988-12-13 1991-10-22 Kansai Paint Co., Ltd. Coating resin composition
US5070174A (en) * 1989-04-28 1991-12-03 The Dow Chemical Company Polyamide epoxy ester resin, process for preparation thereof and coating composition
US5162490A (en) * 1989-06-06 1992-11-10 Schering Ag Polyamide resins based on dimerized fatty acids, process for producing them, and process for manufacturing printing inks by the use of said polyamide resins
US5223558A (en) * 1990-01-22 1993-06-29 The Dow Chemical Company Process for preparation of high-molecular-weight epoxy dimer acid ester resin
EP0555589A1 (en) * 1992-02-10 1993-08-18 Shell Internationale Researchmaatschappij B.V. Vernonia oil modification of epoxy resins
WO1994022954A1 (en) * 1993-03-30 1994-10-13 Shell Internationale Research Maatschappij B.V. Epoxidized vegetable oil modification of epoxy esters
US5391652A (en) * 1992-09-30 1995-02-21 The Dow Chemical Company High molecular weight epoxy ester resin composition, process therefor and coating composition
US5789039A (en) * 1994-09-06 1998-08-04 Herberts Powder Coatings, Inc. Radiation curing of powder coatings on heat sensitive substrates: chemical compositions and processes for obtaining coated workpieces
US5877231A (en) * 1994-04-20 1999-03-02 Herberts Powder Coatings, Inc. Radiation curable powder coatings for heat sensitive substrates
WO2000000533A1 (en) * 1998-06-26 2000-01-06 Vantico Ag Heat-curable can-coating lacquer
KR100587480B1 (en) * 2005-05-06 2006-06-09 국도화학 주식회사 Epoxy modified with alcoxysilane
US20070298976A1 (en) * 2006-06-09 2007-12-27 David Antony Ballard Surfactant materials and coatings for weighting agents for use in oil based drilling fluids
US20110039981A1 (en) * 2008-05-22 2011-02-17 Hefner Robert E Epoxy resins derived from non-seed oil based alkanolamides and a process for preparing the same
US20110046321A1 (en) * 2008-05-22 2011-02-24 Earls Jim D Adducts of epoxy resins derived from alkanolamides and a process for preparing the same
US20110060076A1 (en) * 2008-05-22 2011-03-10 Hefner Jr Robert E Epoxy resins derived from seed oil based alkanolamides and a process for preparing the same
CN104364288A (en) * 2012-06-11 2015-02-18 陶氏环球技术有限公司 Low-viscosity phenolic diglycidyl ethers for epoxy coating applications
WO2023034101A1 (en) 2021-09-01 2023-03-09 Ingevity South Carolina, Llc Bio-based resin, curable composition and polyurethane based thereon, and related methods
US11802176B2 (en) 2019-11-08 2023-10-31 Ingevity South Carolina, Llc Bio-based epoxy resins, compositions, and methods thereof

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3138566A (en) * 1960-01-08 1964-06-23 Gen Mills Inc Fluid resins prepared from epoxidized unsaturated fatty acids or esters
US3351574A (en) * 1965-02-24 1967-11-07 Celanese Coatings Co Castor oil polyglycidyl ether
US4040994A (en) * 1976-11-26 1977-08-09 Unitech Chemical Inc. Cured epoxy resins

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3138566A (en) * 1960-01-08 1964-06-23 Gen Mills Inc Fluid resins prepared from epoxidized unsaturated fatty acids or esters
US3351574A (en) * 1965-02-24 1967-11-07 Celanese Coatings Co Castor oil polyglycidyl ether
US4040994A (en) * 1976-11-26 1977-08-09 Unitech Chemical Inc. Cured epoxy resins

Cited By (23)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5059293A (en) * 1988-12-13 1991-10-22 Kansai Paint Co., Ltd. Coating resin composition
EP0379943A2 (en) * 1989-01-23 1990-08-01 The Dow Chemical Company Process for preparation of high-molecular-weight epoxy dimer acid ester resin
EP0379943A3 (en) * 1989-01-23 1990-11-28 The Dow Chemical Company Process for preparation of high-molecular-weight epoxy dimer acid ester resin
US5070174A (en) * 1989-04-28 1991-12-03 The Dow Chemical Company Polyamide epoxy ester resin, process for preparation thereof and coating composition
US5162490A (en) * 1989-06-06 1992-11-10 Schering Ag Polyamide resins based on dimerized fatty acids, process for producing them, and process for manufacturing printing inks by the use of said polyamide resins
US5223558A (en) * 1990-01-22 1993-06-29 The Dow Chemical Company Process for preparation of high-molecular-weight epoxy dimer acid ester resin
EP0555589A1 (en) * 1992-02-10 1993-08-18 Shell Internationale Researchmaatschappij B.V. Vernonia oil modification of epoxy resins
US5391652A (en) * 1992-09-30 1995-02-21 The Dow Chemical Company High molecular weight epoxy ester resin composition, process therefor and coating composition
WO1994022954A1 (en) * 1993-03-30 1994-10-13 Shell Internationale Research Maatschappij B.V. Epoxidized vegetable oil modification of epoxy esters
CN1046749C (en) * 1993-03-30 1999-11-24 国际壳牌研究有限公司 Epoxidized vegetable oil modification of epoxy esters
US5877231A (en) * 1994-04-20 1999-03-02 Herberts Powder Coatings, Inc. Radiation curable powder coatings for heat sensitive substrates
US5935661A (en) * 1994-09-06 1999-08-10 Herberts Powder Coatings, Inc. Radiation curing of powder coatings on heat sensitive substrates: chemical compositions and processes for obtaining coated workpieces
US5789039A (en) * 1994-09-06 1998-08-04 Herberts Powder Coatings, Inc. Radiation curing of powder coatings on heat sensitive substrates: chemical compositions and processes for obtaining coated workpieces
WO2000000533A1 (en) * 1998-06-26 2000-01-06 Vantico Ag Heat-curable can-coating lacquer
KR100587480B1 (en) * 2005-05-06 2006-06-09 국도화학 주식회사 Epoxy modified with alcoxysilane
US20070298976A1 (en) * 2006-06-09 2007-12-27 David Antony Ballard Surfactant materials and coatings for weighting agents for use in oil based drilling fluids
US8178475B2 (en) * 2006-06-09 2012-05-15 M-I L.L.C Surfactant materials and coatings for weighting agents for use in oil based drilling fluids
US20110039981A1 (en) * 2008-05-22 2011-02-17 Hefner Robert E Epoxy resins derived from non-seed oil based alkanolamides and a process for preparing the same
US20110046321A1 (en) * 2008-05-22 2011-02-24 Earls Jim D Adducts of epoxy resins derived from alkanolamides and a process for preparing the same
US20110060076A1 (en) * 2008-05-22 2011-03-10 Hefner Jr Robert E Epoxy resins derived from seed oil based alkanolamides and a process for preparing the same
CN104364288A (en) * 2012-06-11 2015-02-18 陶氏环球技术有限公司 Low-viscosity phenolic diglycidyl ethers for epoxy coating applications
US11802176B2 (en) 2019-11-08 2023-10-31 Ingevity South Carolina, Llc Bio-based epoxy resins, compositions, and methods thereof
WO2023034101A1 (en) 2021-09-01 2023-03-09 Ingevity South Carolina, Llc Bio-based resin, curable composition and polyurethane based thereon, and related methods

Also Published As

Publication number Publication date
CA1328529C (en) 1994-04-12

Similar Documents

Publication Publication Date Title
US4786666A (en) Epoxy compositions containing glycidyl ethers of fatty esters
EP0692000B1 (en) Epoxidized vegetable oil modification of epoxy esters
US4425451A (en) Epoxy-phosphate aqueous dispersions
US2493486A (en) Tall oil esters
US2759901A (en) Partial esters of epoxide resins
US4119595A (en) Low-temperature epoxy baking compositions
CA1203344A (en) Advancement catalysts for epoxy resins
US3632836A (en) Solid curable polyepoxides modified with hydrolyzed liquid polyepoxides
US6150458A (en) Process for preparing esters of (meth) acrylic acid
US2504518A (en) Synthetic drying compositions
US2653141A (en) Partial esters of polyhydroxyl polyethers
KR970004670B1 (en) Cross-linking agent and curable composition
GB2034319A (en) Water-soluble paint binders
US5760108A (en) Self-dispersing curable epoxy resin esters, dispersions thereof and coating compositions made therefrom
US3507819A (en) Catalytic esterification of epoxy resins
US2908660A (en) Polyepoxide polyalkylene glycol-anhydride compositions and processes for their preparation
US2887459A (en) Mixed resinous esters of oil-modified alkyd resins and of partially-esterified epoxide resins
AU669261B2 (en) Aqueous epoxy resin dispersions
US6673877B2 (en) Product A'ABC of epoxy resins A' and product of polyepoxides A, fatty acids B and amines C
EP0555589B1 (en) Vernonia oil modification of epoxy resins
US2709690A (en) Epoxy resins esterified with drying oil fatty acids and phosphoric acid
US3787508A (en) Solid,curable polyepoxides modified with hydrolyzed liquid polyepoxides
US3397160A (en) Polyurethane modified epoxy esters
US3658738A (en) Water-thinnable paint binders and the preparation thereof
US3477974A (en) Process for the preparation of ester resins

Legal Events

Date Code Title Description
AS Assignment

Owner name: INTEREZ, INC., A CORP. OF GA,KENTUCKY

Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNORS:CECIL, JOSEPH L.;KURNIK, WALTER J.;BABCOCK, DONALD E.;SIGNING DATES FROM 19871116 TO 19871118;REEL/FRAME:004782/0499

Owner name: INTEREZ, INC., 10100 LINN STATION RD., LOUISVILLE,

Free format text: ASSIGNMENT OF ASSIGNORS INTEREST.;ASSIGNORS:CECIL, JOSEPH L.;KURNIK, WALTER J.;BABCOCK, DONALD E.;REEL/FRAME:004782/0499;SIGNING DATES FROM 19871116 TO 19871118

FEPP Fee payment procedure

Free format text: PAYOR NUMBER ASSIGNED (ORIGINAL EVENT CODE: ASPN); ENTITY STATUS OF PATENT OWNER: LARGE ENTITY

FPAY Fee payment

Year of fee payment: 4

AS Assignment

Owner name: HI-TEK POLYMERS, INC. A CORP. OF GA

Free format text: MERGER;ASSIGNOR:INTEREZ, INC. (MERGED INTO);REEL/FRAME:006136/0781

Effective date: 19880725

Owner name: HI-TEK POLYMERS, INC., KENTUCKY

Free format text: MERGER;ASSIGNOR:INTEREZ, INC.;REEL/FRAME:006136/0781

Effective date: 19880725

AS Assignment

Owner name: SHELL OIL COMPANY, TEXAS

Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNOR:HI-TEK POLYMERS, INC.;REEL/FRAME:007082/0029

Effective date: 19930330

REMI Maintenance fee reminder mailed
LAPS Lapse for failure to pay maintenance fees
FP Lapsed due to failure to pay maintenance fee

Effective date: 19961127

STCH Information on status: patent discontinuation

Free format text: PATENT EXPIRED DUE TO NONPAYMENT OF MAINTENANCE FEES UNDER 37 CFR 1.362